US20160126509A1 - Plasma coating for corrosion protection of light-metal components in battery fabrication - Google Patents

Plasma coating for corrosion protection of light-metal components in battery fabrication Download PDF

Info

Publication number
US20160126509A1
US20160126509A1 US14/895,282 US201314895282A US2016126509A1 US 20160126509 A1 US20160126509 A1 US 20160126509A1 US 201314895282 A US201314895282 A US 201314895282A US 2016126509 A1 US2016126509 A1 US 2016126509A1
Authority
US
United States
Prior art keywords
container
elements
cell
lithium
anode
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Abandoned
Application number
US14/895,282
Other languages
English (en)
Inventor
Xiaohong Q. Gayden
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
GM Global Technology Operations LLC
Original Assignee
GM Global Technology Operations LLC
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by GM Global Technology Operations LLC filed Critical GM Global Technology Operations LLC
Publication of US20160126509A1 publication Critical patent/US20160126509A1/en
Abandoned legal-status Critical Current

Links

Images

Classifications

    • H01M2/024—
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00—Secondary cells; Manufacture thereof
    • H01M10/05—Accumulators with non-aqueous electrolyte
    • H01M10/052—Li-accumulators
    • H01M10/0525—Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00—Secondary cells; Manufacture thereof
    • H01M10/05—Accumulators with non-aqueous electrolyte
    • H01M10/058—Construction or manufacture
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00—Secondary cells; Manufacture thereof
    • H01M10/05—Accumulators with non-aqueous electrolyte
    • H01M10/058—Construction or manufacture
    • H01M10/0587—Construction or manufacture of accumulators having only wound construction elements, i.e. wound positive electrodes, wound negative electrodes and wound separators
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/10—Primary casings; Jackets or wrappings
    • H01M50/116—Primary casings; Jackets or wrappings characterised by the material
    • H01M50/117—Inorganic material
    • H01M50/119—Metals
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/10—Primary casings; Jackets or wrappings
    • H01M50/116—Primary casings; Jackets or wrappings characterised by the material
    • H01M50/121—Organic material
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/10—Primary casings; Jackets or wrappings
    • H01M50/116—Primary casings; Jackets or wrappings characterised by the material
    • H01M50/124—Primary casings; Jackets or wrappings characterised by the material having a layered structure
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/10—Primary casings; Jackets or wrappings
    • H01M50/116—Primary casings; Jackets or wrappings characterised by the material
    • H01M50/124—Primary casings; Jackets or wrappings characterised by the material having a layered structure
    • H01M50/1245—Primary casings; Jackets or wrappings characterised by the material having a layered structure characterised by the external coating on the casing
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/10—Primary casings; Jackets or wrappings
    • H01M50/14—Primary casings; Jackets or wrappings for protecting against damage caused by external factors
    • H01M50/145—Primary casings; Jackets or wrappings for protecting against damage caused by external factors for protecting against corrosion
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D1/00—Processes for applying liquids or other fluent materials
    • B05D1/62—Plasma-deposition of organic layers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D2202/00—Metallic substrate
    • B05D2202/20—Metallic substrate based on light metals
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D5/00—Processes for applying liquids or other fluent materials to surfaces to obtain special surface effects, finishes or structures
    • B05D5/08—Processes for applying liquids or other fluent materials to surfaces to obtain special surface effects, finishes or structures to obtain an anti-friction or anti-adhesive surface
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2220/00—Batteries for particular applications
    • H01M2220/20—Batteries in motive systems, e.g. vehicle, ship, plane
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/10—Primary casings; Jackets or wrappings
    • H01M50/102—Primary casings; Jackets or wrappings characterised by their shape or physical structure
    • H01M50/103—Primary casings; Jackets or wrappings characterised by their shape or physical structure prismatic or rectangular
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10—Energy storage using batteries
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T10/00—Road transport of goods or passengers
    • Y02T10/60—Other road transportation technologies with climate change mitigation effect
    • Y02T10/70—Energy storage systems for electromobility, e.g. batteries

Definitions

  • This invention pertains to the coating of prismatic aluminum or magnesium containers for lithium-ion battery cell materials to protect the light-weight metal from salt water corrosion and to provide electrical insulation between touching containers when they get wet in service. More specifically, a coating material and an atmospheric plasma coating process is provided that may be used to coat the aluminum or magnesium containers in an ambient atmosphere and at a relatively low temperature after they have been filled with their heat-sensitive electrode and electrolyte constituents. The practice of this invention is particularly useful for lithium-ion battery assemblies used on automotive vehicles or other applications in which the light-metal battery containers may be exposed to water-containing corrosive salts or the like.
  • Assemblies of lithium-ion battery cells are finding increasing applications in providing motive power in automotive vehicles.
  • Each cell of the battery is capable of providing an electrical potential of about three to four volts and a direct electrical current based on the composition and mass of the electrode materials in the cell.
  • the cell is capable of being discharged and re-charged over many cycles.
  • a battery is assembled for an application by combining a suitable number of individual cells in a combination of electrical parallel and series connections to satisfy voltage and current requirements for a specified electric motor.
  • the assembled battery may, for example, comprise up to three hundred individually packaged cells that are electrically interconnected to provide forty to four hundred volts and sufficient electrical power to an electrical traction motor to drive a vehicle.
  • the direct current produced by the battery may be converted into an alternating current for more efficient motor operation.
  • the batteries may be used as the sole motive power source for electric motor driven electric vehicles or as a contributing power source in various types of hybrid vehicles, powered by a combination of an electric motor(s) and hydrocarbon-fueled engine.
  • an electric motor(s) and hydrocarbon-fueled engine powered by a combination of an electric motor(s) and hydrocarbon-fueled engine.
  • Lithium-ion batteries for powering automotive vehicles are typically assembled using cans of individual cells. That is, each cell has its own can, enclosing the material elements of a lithium-ion cell with electrically conductive electrode tabs (terminals) extending from each cell container for interconnection with the electrode tabs of another cell or cells.
  • a number of cell cans for example twelve or twenty-four cell cans, are often grouped and interconnected as a “module”.
  • a number of modules, or the like, are assembled into “packs” of a desired voltage and current producing capability.
  • the shapes of the cell cans are often prismatic, with six rectangular sides and bases, for assembly and support of the modules. The cans add weight to the assembled battery and to the vehicle that the battery serves.
  • the material of the cans must provide strength for the assembly and containment of the cell components, and the cans must enable cooling of the battery cells because the electrochemical cells produce considerable heat in their use.
  • the lithium-ion battery assembly is often located low in the vehicle body structure where it may be exposed to external corrosive materials from road surfaces.
  • the cans have been made of steel for strength, heat transfer, and resistance to salt water. But steel is relatively heavy. There is a need to adapt lighter metals for use in the assembly of lithium-ion battery cells intended for automotive applications.
  • a suitable aluminum alloy or magnesium alloy material is formed into a suitable thin-wall container shape(s) for insertion of the elements of a lithium-ion cell.
  • the shapes of the containers are often prismatic and they are called cans.
  • the cans are typically formed with a removed (or removable) side (or top) so that preformed electrode materials and separator materials may be placed in an open-side can.
  • a multi-step procedure is involved in the placement of the electrode materials, separators, and the electrolyte in the can, the welding of electrode tabs to terminals on the can for interconnection with other cans, and the like, as will be described in more detail below in this specification.
  • a silicone polymer-containing coating is applied to outside surfaces of the can (and optionally to inside surfaces) to protect the light weight aluminum or magnesium from salt water or other corrosive environmental materials.
  • the coating process uses hexamethyldisiloxane (HMDSO) as the starting material and it is applied to surfaces of the light-metal can by a low temperature atmospheric plasma process.
  • HMDSO hexamethyldisiloxane
  • the liquid HMDSO is delivered to a plasma nozzle (commercially available) in which it is vaporized in an air-plasma stream and directed against surfaces of the aluminum or magnesium can with its lithium-ion cell material contents.
  • the material is delivered through the plasma nozzle onto all external surfaces of the can to form a coextensive coating of polymerized hexamethyldisiloxane, typically a silicone polymer.
  • 1 to about one to about three micrometers is generally suitable to protect the light-metal can material from corrosive elements encountered in vehicle operation.
  • the coating is hydrophobic to shield the cell can surfaces from ambient water and also provides an electrical insulation layer on touching cell can surfaces to electrically isolate them, especially in the presence of water.
  • the protective coating may be robotically applied (for example) to the aluminum or magnesium can surface at any of several different steps or locations in a manufacturing line in which lithium-ion cell elements are being placed in the can, or electrode connections are being made with terminals on the can, or the electrolyte is being inserted into the can, or upon can closure, cell activation, can sealing, cell can testing, or other processing of the lithium-ion cell can that is being preformed.
  • a durable hydrophobic, silicone-type polymer coating may be applied to surfaces of the light metal can as the cell is being made and assembled, and the coating may be applied and formed without damage to the vital constituents within the container to which it is applied.
  • inside surfaces of the can may be coated before active elements of the cell are inserted.
  • the outer surfaces of the can may be coated before the can is delivered to the in-line operation in which the cell elements are assembled in the light-metal can. But it is preferred that outer surfaces be coated at a predetermined step in an in-line type assembly and fabrication of the cell elements and their placement in the light-metal container in which they are to be used in the vehicle battery.
  • the drawing FIGURE is an oblique view of an upstanding aluminum or magnesium can, with a portion of a major side face removed, showing the placement of a roll of layered lithium-ion single-cell elements in the container.
  • a coating of polymerized hexamethyldisiloxane is to be applied to each of the outer surfaces of the can using, for example, a computer-controlled, robot-carried nozzle for generating atmospheric pressure plasma of the disiloxane in air and applying a silicone-based coating to surfaces of the light-metal container of the cell materials.
  • This invention pertains to the manufacture of lithium-ion electrochemical cells for automotive vehicle batteries, particularly for applications in which the battery is to be located on the vehicle where cells (or cans of individual cells) may be exposed to road-splash salty water or other corrosive water compositions.
  • the electrode and separator elements of each cell are usually separately formed, assembled in a suitable cell arrangement, and placed into a pre-formed, partly opened, container body or can.
  • the container cans are often prismatic in shape, with three sets of opposing rectangular sides, so that many cans can be placed together and electrically interconnected to form a vehicle battery.
  • two to three hundred, substantially identical, single-cells are joined in I or T shaped arrangements and placed on a complementary support tray or plate, carried on a structural member of the vehicle body.
  • means is provided for water cooling (or water-glycol cooling) of the many cell cans because they generate heat as they are discharged and re-charged.
  • the cooling conduits are formed in, or as part of, the cans.
  • the container bodies have been made of steel, or of a suitable polymer composition (or polymer/metal foil laminate), in order to resist ambient salt water corrosion. But the polymeric materials do not readily conduct heat away from the operating lithium-ion cells, and steel is relatively heavy.
  • the purpose of the subject invention is to adapt light-metal container materials, such as aluminum or aluminum alloys or magnesium or its alloys, for use as can material or container material for individual lithium-ion cells.
  • a silicone polymer coating is formed on surfaces of the light-metal cell can by application of hexamethyldisiloxane using a low temperature, atmospheric plasma spray process.
  • the resulting silicone polymer coating provides good protection against water-based corrosion of the aluminum or magnesium cans making up the battery assembly.
  • the silicone coating is formed on surfaces of the aluminum or magnesium cans during the in-line assembly/manufacturing process in which electrode-current conductor elements, separator elements, and the electrolyte are being assembled and fitted into their rectangular prismatic containers.
  • the drawing FIGURE illustrates an exemplary prismatic rectangular cell can 10 with six thin wall sides formed of a suitable aluminum or magnesium alloy.
  • the shape of the cell can enables it to be placed against like-shaped cell cans in assembling cell modules and the like.
  • the front-facing major vertical side 12 of cell-can 10 is largely broken away to show an assembled roll 14 of the solid elements of the single-cell.
  • the rear major vertical side of cell can 10 is the same size and shape as front-facing side 12 , but the rear side is hidden in this view.
  • One vertical edge side 16 is visible and the opposing, like-shaped vertical edge side is hidden.
  • the bottom surface of cell can 10 is hidden and the top side 18 is shown in a position separated and elevated from the sides 12 , 16 of cell can 10 .
  • the top side 18 of cell can 10 is not joined to the remainder of the cell can structure until assembled roll 14 of the solid elements of the cell has been placed in the open-top can.
  • the assembled roll 14 of thin-layer cell elements consists of a single, relatively long layer of anode elements 20 , a long separator layer 22 , a single, relatively long layer of cathode elements 24 , and another long separator layer 22 .
  • the layer of anode elements 20 will have at least one electrical connector tab 26 , located along its length, for welding to a terminal 28 on the top side 18 of the can 10 .
  • the layer of cathode elements 24 will have at least one tab 30 , suitably located along its length, for connection to a terminal 32 on the top side 18 of cell can 10 .
  • the top side 18 of cell can 10 may also have a small opening 34 for injection of a liquid electrolyte into the assembled roll 14 of cell elements after the top side 18 has been welded (or otherwise fixed) to the vertical sides 12 , 16 of cell can 10 . Opening 34 in top side 18 will be closed after the electrolyte has been added to the other cell elements (roll 14 ).
  • each of the outer surfaces (including visible surfaces 12 , 16 , and 18 ) of the cell can 10 will be coated with a layer (e.g., up to about one micrometer or more in thickness) of silicone polymer (or silicone-type polymer) by an atmospheric plasma spray method using hexamethyldisiloxane.
  • a layer e.g., up to about one micrometer or more in thickness
  • Plasma spray methods and plasma spray nozzles are known and commercially available.
  • the initially liquid hexamethyldisiloxane is suitably introduced into and carried in a confined stream of air (for example) into a plasma nozzle in which the air is converted to a plasma stream at atmospheric pressure.
  • the stream of air-based plasma-disiloxane material is progressively directed by the nozzle against surfaces of the aluminum or magnesium cell container.
  • the disiloxane material is deposited on the surfaces of the container, where it polymerizes into a hydrophobic, protective layer of silicone material.
  • Such plasma nozzles for this application are commercially available and may be carried and used on robot arms, under multi-directional computer control, to coat the many surfaces of each can for a lithium-ion cell module.
  • the plasma nozzle typically has a metallic tubular housing which provides a flow path of suitable length for receiving the flow of working gas and hexamethyldisiloxane precursor material and for enabling the formation of the plasma stream in an electromagnetic field established within the flow path of the tubular nozzle.
  • the tubular housing terminates in a conically tapered outlet, shaped to direct the shaped plasma stream toward an intended workpiece.
  • An electrically insulating ceramic tube is typically inserted at the inlet of the tubular housing such that it extends along a portion of the flow passage.
  • a stream of a working gas, such as air, and carrying dispersed droplets of hexamethyldisiloxane, is introduced into the inlet of the nozzle.
  • the flow of the air-disiloxane mixture may be caused to swirl turbulently in its flow path by use of a swirl piece with flow openings, also inserted near the inlet end of the nozzle.
  • a linear (pin-like) electrode is placed at the ceramic tube site, along the flow axis of the nozzle at the upstream end of the flow tube.
  • the electrode is powered by a high frequency generator at a frequency of about 50 to 60 kHz (for example) and to a suitable potential of a few kilovolts.
  • the metallic housing of the plasma nozzle is grounded. Thus, an electrical discharge can be generated between the axial pin electrode and the housing.
  • the frequency of the applied voltage and the dielectric properties of the ceramic tube produce a corona discharge at the stream inlet and the electrode.
  • an arc discharge from the electrode tip to the housing is formed.
  • This arc discharge is carried by the turbulent flow of the air/hexamethyldisiloxane stream to the outlet of the nozzle.
  • a reactive plasma of the air and disiloxane mixture is formed at a relatively low temperature.
  • a copper nozzle at the outlet of the nozzle is shaped to direct the plasma stream in a suitably confined path against the surfaces of an aluminum or magnesium can for the lithium-ion cell elements.
  • the plasma nozzle may be carried by a computer-controlled robot to move the plasma stream in multi-directional paths over each surface of the light-metal can to deposit the disiloxane material in a continuous thin layer on the container.
  • the deposited plasma-activated material forms a hydrophobic silicone polymer layer on the container of the lithium-cell elements that provides resistance to water-based corrosion of the can.
  • the coating needs to be free of pinholes or other like defects. The coating must serve to prevent water from contacting the aluminum or magnesium surface and the coating serves as an electrical insulator between cell cans, especially in the presence of water. In general, it is preferred that the coating be applied to each outer surface of the light metal container (and, optionally, to the internal surfaces of the container).
  • This coating process is preferably conducted at one or more of the processing stages in which layered electrode and separator cell elements have been placed in the cell can and are being connected to it and closed within the can.
  • This plasma coating process may be conducted so as to avoid thermal damage to the heat-sensitive elements of the lithium-ion cell.
  • the electrode, separator, and electrolyte elements of a specified lithium-ion cell are typically prepared separately and brought together in the manufacturing process by which each cell is made. An illustration of one common such group of cell elements will be described.
  • the negative electrode (anode, during cell discharge) is often formed by depositing a thin layer of graphite, optionally mixed with conductive carbon black, and a suitable polymeric binder onto a thin foil of copper which serves as the current collector for the negative electrode.
  • the metal current collector may be formed with one or more tabs for making electrical connections with a negative terminal on the cell can.
  • This mixture of bonded, graphitic electrode material is porous, so as to permit suitable infiltration of the non-aqueous electrolyte with its dissolved lithium ions which are intercalated as lithium into the graphitic carbon during activation or charging of the cell.
  • lithium ions flow from the negative electrode material through the electrolyte and into the positive electrode (cathode, during cell discharge).
  • the negative electrode is typically initially formed as a thin sheet layer of less than one millimeter (e.g., a few hundred micrometers) or so in thickness.
  • the original sheet of electrode material may be formed of a size for manufacturing efficiency. Smaller portions, for specific electrode designs, may be cut from the initial sheet for a layered assembly of the electrode material with other elements of cell.
  • Such a layer of negative electrode (or anode material) is illustrated at 20 in the drawing FIGURE.
  • the positive electrode is also a thin layer of a porous particulate metal oxide composition, which is suitably bonded to a thin foil of aluminum which serves as the current collector for the positive electrode.
  • the aluminum foil may be formed with one or more tabs for connection with a positive terminal on the cell can.
  • lithium ions flow through the electrolyte and intercalate into the metal oxide composition.
  • metal oxides for the positive electrode include LiMnO 2 , LiMn 2 O 4 , LiNiO 2 , and LiCoO 2 .
  • the metal oxide particles are secured as a porous layer to the current collector foil with a suitable organic polymer binder that bonds the particles without inhibiting electrolyte penetration and contact with them.
  • the positive electrode material is formed as a thin layer of material and is illustrated ( 24 ) in the drawing FIGURE.
  • shape and dimensions of the positive electrode/current collector layer would generally be determined to complement the shape and dimensions of the negative electrode layer, and an interposed separator layer.
  • a thin porous separator layer is interposed between the negative electrode layer and the positive electrode layer.
  • the separator material is a porous layer of polyethylene or polypropylene.
  • the thermoplastic material comprises interbonded fibers of PE or PP.
  • the fiber surfaces of the layer may be coated with particles of alumina, or the like, to enhance the electrical resistance of the separator, while retaining the porosity of the separator for infiltration with liquid electrolyte and transport of lithium ions between the cell electrodes.
  • the separator layer is used to prevent direct electrical contact between the negative and positive electrode layers, and is shaped and sized to serve this function.
  • the electrolyte for the lithium-ion cell is often a lithium salt dissolved in one or more organic liquid solvents.
  • salts include lithium hexafluorophosphate (LiPF 6 ), lithium tetrafluoroborate (LiBF 4 ), lithium perchlorate (LiClO 4 ), lithium hexafluoroarsenate (LiAsF 6 ), and lithium trifluoroethanesulfonimide.
  • Some examples of solvents that may be used to dissolve the electrolyte salt include ethylene carbonate, dimethyl carbonate, methylethyl carbonate, propylene carbonate. There are other lithium salts that may be used and other solvents.
  • a combination of lithium salt and solvent is selected for providing suitable mobility and transport of lithium ions in the operation of the cell.
  • the electrolyte is carefully dispersed into and between closely spaced layers of the electrode elements and separator layers.
  • the electrolyte is not illustrated in the drawing FIGURE because it is difficult to illustrate between tightly rolled layers and because, in many embodiments, it has not been inserted with the other electrode materials until the top surface 18 has been welded onto the remainder to the cell can.
  • lithium-ion electrochemical cells may be formed using many different shapes and sizes of the negative and positive electrodes to serve a specific power providing function.
  • the shape of the can or container may be modified in some respect to accommodate the flow of air or a liquid coolant into heat transfer contact with one or more surfaces of the can, but not with the contained elements of the lithium-ion cell.
  • the coolant is often water or a water-glycol mixture.
  • other structural coolant passages are formed and assembled against surfaces of a pack of cell modules.
  • each cell in a suitable can or container.
  • Each cell can or container has at least one external terminal for each of the negative electrode and the positive electrode.
  • each cell can have a rectangular shape to easily permit many cans being stacked in a packed structure to form a specified battery or portion of a battery. Appropriate electrical connections are made between the terminals of adjoining cell-cans in order to provide a desired or specified voltage and current output potential for an assembled battery structure.
  • the cans containing the cell elements are formed of aluminum or magnesium (or their alloys) and the external surfaces (at least) are coated with a silicone polymer at an appropriate stage, such as (i) after the loading of the solid, layered, cell elements into the can, (ii) the welding of electrode current collector tabs to a can member or surface, (iii) the injection or loading of the electrolyte into the cans and into (onto) the elements of the caned cell, and/or (iv) the formation of the cell or the sealing of the can.
  • a silicone polymer such as (i) after the loading of the solid, layered, cell elements into the can, (ii) the welding of electrode current collector tabs to a can member or surface, (iii) the injection or loading of the electrolyte into the cans and into (onto) the elements of the caned cell, and/or (iv) the formation of the cell or the sealing of the can.
  • liquid hexamethyldisiloxane is dispersed in an atmospheric air plasma stream and applied to surfaces of the can at one or more of these stages during filling of the cell elements into a previously formed can member, closure of the can container, and testing and acceptance of the cell.
  • the coating self-cures as a thin protective silicone polymer layer (up to about one micrometer or more in thickness) on exposed surfaces of the cell container.
  • strips of anode material (aka negative electrode material, 20 in drawing FIGURE), cathode material (positive electrode, 24 ), and separator material ( 22 ) are delivered in parallel flow paths for the assembly of these solid cell elements into overlying layers for rolling or folding (roll 14 ) and placing into a suitably sized light-metal can 10 , also carried to the assembly site.
  • the respective thin strip electrode elements and separator thin strip element are generally rectangular in shape and have been trimmed to their respective lengths and widths for their assembly and placement in the aluminum or magnesium can.
  • One or more thin metal electrode tabs have been formed or placed in or on the metal foil current collector foil of each electrode layer (e.g., 26 , 30 in drawing FIGURE).
  • a four layer assembly may be formed with an anode layer, a separator layer, a cathode layer, and a second separator layer assembly as illustrated (at 14 ) in the drawing FIGURE.
  • five layer assemblies are prepared an anode-separator-cathode-separator-anode arrangement or with a cathode-separator- anode-separator- cathode arrangement. These arrangements are usually specified based on the respective material loadings and electrochemical current capacities of the respective electrode material selections. These assembled layers are then rolled or folded so as to be placed in the intended opened aluminum or magnesium can.
  • both terminals ( 28 , 32 are located at the same surface (top surface 18 ) of the metal container 10 .
  • the dry elements are placed in their container with suitable electrical connections between the electrode elements and the positive electrode and negative electrode terminals on the can.
  • the welded connections may be made to terminals on a free-standing top surface of the can.
  • the top-side may then be welded to vertical sides of the cell can.
  • the can is, for example, thus closed and suitably sealed around the enclosed elements.
  • the plasma coating may now be applied to each of the external surfaces of the metal can. But there are further stages in the assembly process and further opportunities for the application of the atmospheric plasma coating.
  • a small opening e.g., 34 in top side 18
  • the coating of the outside surfaces of the light metal container may be done following the insertion of the liquid electrolyte.
  • the cell may now be activated by applying an electrical potential between its terminals to intercalate lithium ions into the anode material (first charging cycle).
  • the cell may then be partially discharged through a suitable external resistance to further the activation of the cell elements.
  • This charging-discharging practice may be repeated a few times to complete cell module activation and “age” the active elements of the cell.
  • Atmospheric plasma coating using hexamethyldisiloxane may be performed during or after such activation procedures.
  • the cell is now ready for further assembly with a specified number of other, like-prepared and coated cell cans.
  • a collection of coated lithium-ion cells will eventually be placed on a suitable tray or other support structure to form one of the battery modules in an automotive battery pack.
  • a tray or other support structure may also be coated with a film of silicone polymer by the subject process.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Inorganic Chemistry (AREA)
  • Secondary Cells (AREA)
  • Battery Mounting, Suspending (AREA)
  • Sealing Battery Cases Or Jackets (AREA)
  • Connection Of Batteries Or Terminals (AREA)
US14/895,282 2013-06-04 2013-06-04 Plasma coating for corrosion protection of light-metal components in battery fabrication Abandoned US20160126509A1 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/CN2013/076700 WO2014194466A1 (fr) 2013-06-04 2013-06-04 Revêtement au plasma pour la protection contre la corrosion d'éléments en métaux légers dans la fabrication de batteries

Publications (1)

Publication Number Publication Date
US20160126509A1 true US20160126509A1 (en) 2016-05-05

Family

ID=52007395

Family Applications (1)

Application Number Title Priority Date Filing Date
US14/895,282 Abandoned US20160126509A1 (en) 2013-06-04 2013-06-04 Plasma coating for corrosion protection of light-metal components in battery fabrication

Country Status (4)

Country Link
US (1) US20160126509A1 (fr)
CN (1) CN105531841A (fr)
DE (1) DE112013007033T5 (fr)
WO (1) WO2014194466A1 (fr)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109487258A (zh) * 2019-01-10 2019-03-19 西安交通大学 一种通过低温等离子体制备的镁锂合金高耐蚀无机膜层及方法
CN111066171A (zh) * 2017-09-04 2020-04-24 罗伯特·博世有限公司 具有隔离层的电池组电池
US11329339B2 (en) * 2018-05-03 2022-05-10 Robert Bosch Gmbh Method for manufacturing a battery cell with an oxygen diffusion barrier layer
CN116657074A (zh) * 2023-05-25 2023-08-29 江苏风驰碳基新材料研究院有限公司 一种钠离子电池生产用外表面处理装置

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105957985B (zh) * 2016-07-18 2018-09-25 南京楚卿电子科技有限公司 一种具有耐腐蚀性能的蓄电池
WO2020041375A1 (fr) * 2018-08-21 2020-02-27 Richard Theodore Wurden Batteries pour systèmes de propulsion marine électriques et systèmes et procédés associés
CN109860446A (zh) * 2019-03-07 2019-06-07 拓米(成都)应用技术研究院有限公司 用于封装薄膜锂电池的三明治结构复合薄膜及其制备方法
EP3806179B1 (fr) * 2019-10-10 2024-03-20 VARTA Microbattery GmbH Batterie lithium secondaire et procédé de fabrication
CN115411420A (zh) * 2021-05-26 2022-11-29 江苏菲沃泰纳米科技股份有限公司 一种具有涂层的电池及其制备方法
DE102021207108A1 (de) 2021-07-06 2023-01-12 Volkswagen Aktiengesellschaft Akkumulator für ein Kraftfahrzeug und Verfahren zu dessen Herstellung
WO2023240531A1 (fr) * 2022-06-16 2023-12-21 宁德时代新能源科技股份有限公司 Procédé et dispositif de protection pour batterie secondaire, batterie secondaire, module de batterie, bloc-batterie et dispositif électrique

Family Cites Families (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001283796A (ja) * 2000-04-04 2001-10-12 Matsushita Electric Ind Co Ltd リチウム二次電池とその製造方法
CN1242092C (zh) * 2001-11-19 2006-02-15 乐金电子(天津)电器有限公司 一种利用等离子体技术的金属抗腐蚀处理方法
KR100614372B1 (ko) * 2004-06-25 2006-08-21 삼성에스디아이 주식회사 원통형 리튬 이차 전지 및 그의 제조 방법
US20060147770A1 (en) * 2005-01-04 2006-07-06 Bernd Krause Reduction of voltage loss caused by voltage cycling by use of a rechargeable electric storage device
CN100369314C (zh) * 2005-08-08 2008-02-13 河南环宇集团有限公司 磷酸基锂离子电池的制备方法及其制备的电池
JP5182838B2 (ja) * 2006-07-25 2013-04-17 株式会社デンソー リチウム電池容器用封口板，その製造方法およびリチウム電池
DE102007000611A1 (de) * 2007-10-31 2009-05-07 Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. Kratzfeste und dehnbare Korrosionsschutzschicht für Leichtmetallsubstrate
JP5846032B2 (ja) * 2011-06-07 2016-01-20 日本軽金属株式会社 成形性、溶接性に優れた電池ケース用アルミニウム合金板
CN102354732A (zh) * 2011-09-24 2012-02-15 李其真 一种汽车动力电池外壳的制造工艺
CN202405330U (zh) * 2011-12-27 2012-08-29 青岛海霸能源集团有限公司 圆柱型锂离子电池的壳体结构

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111066171A (zh) * 2017-09-04 2020-04-24 罗伯特·博世有限公司 具有隔离层的电池组电池
US11329339B2 (en) * 2018-05-03 2022-05-10 Robert Bosch Gmbh Method for manufacturing a battery cell with an oxygen diffusion barrier layer
CN109487258A (zh) * 2019-01-10 2019-03-19 西安交通大学 一种通过低温等离子体制备的镁锂合金高耐蚀无机膜层及方法
CN116657074A (zh) * 2023-05-25 2023-08-29 江苏风驰碳基新材料研究院有限公司 一种钠离子电池生产用外表面处理装置

Also Published As

Publication number Publication date
DE112013007033T5 (de) 2016-01-21
WO2014194466A1 (fr) 2014-12-11
CN105531841A (zh) 2016-04-27

Similar Documents

Publication Publication Date Title
US20160126509A1 (en) Plasma coating for corrosion protection of light-metal components in battery fabrication
JP4370902B2 (ja) バイポーラ電池およびその製造方法。
US20180048040A1 (en) Capacitor-battery hybrid formed by plasma powder electrode coating
CN101904029B (zh) 具有改进的安全性的袋型二次电池
WO2005013408A1 (fr) Accumulateur au lithium
CN112864546B (zh) 非水电解质二次电池
US20160254569A1 (en) Assembled battery
EP3142173A1 (fr) Électrode positive pour accumulateurs à électrolyte non aqueux et accumulateur à électrolyte non aqueux
CN109585853B (zh) 非水电解质二次电池及其制造方法
US20160254533A1 (en) Making lithium secondary battery electrodes using an atmospheric plasma
JP7085147B2 (ja) 非水電解質二次電池
KR20140033585A (ko) 이차전지
CN103943801A (zh) 具有改进安全特性的原电池
CN111954944A (zh) 非水电解质二次电池的制造方法
KR20160141654A (ko) 리튬 이온 2차 전지
CN111384451A (zh) 层叠体
CN113270571B (zh) 锂离子二次电池的制造方法和负极材料
CN110447120B (zh) 锂离子电池
JP5326450B2 (ja) 電極およびその製造方法
WO2019008546A1 (fr) Procédé de fabrication de corps d'électrode stratifié, et procédé de fabrication d'élément de stockage d'énergie
JP2004319210A (ja) バイポーラ電池、バイポーラ電池の製造方法、組電池および車両
JP6663178B2 (ja) リチウムイオン二次電池
JP4055640B2 (ja) バイポーラ電池、バイポーラ電池の製造方法、組電池および車両
JP5509561B2 (ja) 非水電解質二次電池
JP7377831B2 (ja) 二次電池の集電体および二次電池

Legal Events

Date Code Title Description
STCB Information on status: application discontinuation

Free format text: ABANDONED -- FAILURE TO PAY ISSUE FEE